JPH0733473B2 - Filled polymer blend - Google Patents
Filled polymer blendInfo
- Publication number
- JPH0733473B2 JPH0733473B2 JP2091943A JP9194390A JPH0733473B2 JP H0733473 B2 JPH0733473 B2 JP H0733473B2 JP 2091943 A JP2091943 A JP 2091943A JP 9194390 A JP9194390 A JP 9194390A JP H0733473 B2 JPH0733473 B2 JP H0733473B2
- Authority
- JP
- Japan
- Prior art keywords
- polymer blend
- filler
- rubber
- copolymer
- blend
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 229920002959 polymer blend Polymers 0.000 title claims description 16
- 239000000203 mixture Substances 0.000 claims description 38
- 239000000945 filler Substances 0.000 claims description 28
- 229920001577 copolymer Polymers 0.000 claims description 27
- 239000002245 particle Substances 0.000 claims description 27
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims description 18
- 239000004417 polycarbonate Substances 0.000 claims description 16
- 229920000515 polycarbonate Polymers 0.000 claims description 16
- 229920001971 elastomer Polymers 0.000 claims description 15
- 239000005060 rubber Substances 0.000 claims description 15
- 239000004927 clay Substances 0.000 claims description 14
- 239000000454 talc Substances 0.000 claims description 13
- 229910052623 talc Inorganic materials 0.000 claims description 13
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 claims description 8
- 229920001519 homopolymer Polymers 0.000 claims description 8
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 claims description 6
- 125000003118 aryl group Chemical group 0.000 claims description 5
- 239000000178 monomer Substances 0.000 claims description 5
- 229920002554 vinyl polymer Polymers 0.000 claims description 4
- HIDBROSJWZYGSZ-UHFFFAOYSA-N 1-phenylpyrrole-2,5-dione Chemical compound O=C1C=CC(=O)N1C1=CC=CC=C1 HIDBROSJWZYGSZ-UHFFFAOYSA-N 0.000 claims description 3
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims 1
- 239000005977 Ethylene Substances 0.000 claims 1
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 description 11
- 238000002474 experimental method Methods 0.000 description 9
- 238000000034 method Methods 0.000 description 7
- 229920000642 polymer Polymers 0.000 description 7
- 230000000052 comparative effect Effects 0.000 description 6
- 238000012856 packing Methods 0.000 description 6
- 239000011159 matrix material Substances 0.000 description 5
- 229920002857 polybutadiene Polymers 0.000 description 5
- 239000011347 resin Substances 0.000 description 5
- 229920005989 resin Polymers 0.000 description 5
- 238000010528 free radical solution polymerization reaction Methods 0.000 description 4
- 229920005668 polycarbonate resin Polymers 0.000 description 4
- 239000004431 polycarbonate resin Substances 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 3
- 239000005062 Polybutadiene Substances 0.000 description 3
- 239000000654 additive Substances 0.000 description 3
- 229920000402 bisphenol A polycarbonate polymer Polymers 0.000 description 3
- 239000000839 emulsion Substances 0.000 description 3
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 description 2
- XYLMUPLGERFSHI-UHFFFAOYSA-N alpha-Methylstyrene Chemical compound CC(=C)C1=CC=CC=C1 XYLMUPLGERFSHI-UHFFFAOYSA-N 0.000 description 2
- 229920006125 amorphous polymer Polymers 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 238000012662 bulk polymerization Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000013329 compounding Methods 0.000 description 2
- 238000007720 emulsion polymerization reaction Methods 0.000 description 2
- -1 ethylene, propylene Chemical group 0.000 description 2
- 238000009863 impact test Methods 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 238000001746 injection moulding Methods 0.000 description 2
- 239000011256 inorganic filler Substances 0.000 description 2
- 229910003475 inorganic filler Inorganic materials 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- KYPOHTVBFVELTG-OWOJBTEDSA-N (e)-but-2-enedinitrile Chemical compound N#C\C=C\C#N KYPOHTVBFVELTG-OWOJBTEDSA-N 0.000 description 1
- VEORPZCZECFIRK-UHFFFAOYSA-N 3,3',5,5'-tetrabromobisphenol A Chemical compound C=1C(Br)=C(O)C(Br)=CC=1C(C)(C)C1=CC(Br)=C(O)C(Br)=C1 VEORPZCZECFIRK-UHFFFAOYSA-N 0.000 description 1
- ODJUOZPKKHIEOZ-UHFFFAOYSA-N 4-[2-(4-hydroxy-3,5-dimethylphenyl)propan-2-yl]-2,6-dimethylphenol Chemical compound CC1=C(O)C(C)=CC(C(C)(C)C=2C=C(C)C(O)=C(C)C=2)=C1 ODJUOZPKKHIEOZ-UHFFFAOYSA-N 0.000 description 1
- VOWWYDCFAISREI-UHFFFAOYSA-N Bisphenol AP Chemical compound C=1C=C(O)C=CC=1C(C=1C=CC(O)=CC=1)(C)C1=CC=CC=C1 VOWWYDCFAISREI-UHFFFAOYSA-N 0.000 description 1
- 239000004429 Calibre Substances 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- 238000012695 Interfacial polymerization Methods 0.000 description 1
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 1
- GYCMBHHDWRMZGG-UHFFFAOYSA-N Methylacrylonitrile Chemical compound CC(=C)C#N GYCMBHHDWRMZGG-UHFFFAOYSA-N 0.000 description 1
- 239000006057 Non-nutritive feed additive Substances 0.000 description 1
- YGYAWVDWMABLBF-UHFFFAOYSA-N Phosgene Chemical compound ClC(Cl)=O YGYAWVDWMABLBF-UHFFFAOYSA-N 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 238000003917 TEM image Methods 0.000 description 1
- 239000004433 Thermoplastic polyurethane Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 150000008044 alkali metal hydroxides Chemical class 0.000 description 1
- 125000005250 alkyl acrylate group Chemical group 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 229920001400 block copolymer Polymers 0.000 description 1
- 229920001727 cellulose butyrate Polymers 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000007822 coupling agent Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 125000005028 dihydroxyaryl group Chemical group 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000635 electron micrograph Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 229920000578 graft copolymer Polymers 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000006082 mold release agent Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 150000003961 organosilicon compounds Chemical class 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 229920002587 poly(1,3-butadiene) polymer Polymers 0.000 description 1
- 229920003229 poly(methyl methacrylate) Polymers 0.000 description 1
- 229920001230 polyarylate Polymers 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 239000002952 polymeric resin Substances 0.000 description 1
- 239000004926 polymethyl methacrylate Substances 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 description 1
- 229920005604 random copolymer Polymers 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 235000012424 soybean oil Nutrition 0.000 description 1
- 239000003549 soybean oil Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 229920002803 thermoplastic polyurethane Polymers 0.000 description 1
- 229920005992 thermoplastic resin Polymers 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/20—Compounding polymers with additives, e.g. colouring
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/34—Silicon-containing compounds
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/34—Silicon-containing compounds
- C08K3/346—Clay
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L69/00—Compositions of polycarbonates; Compositions of derivatives of polycarbonates
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Dispersion Chemistry (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
【発明の詳細な説明】 本発明は非晶質ポリマーマトリックスを無機充てん剤と
から成る新規なポリマー成形組成物(polymeric moldin
g composition)に関する。さらに詳しくは、本発明は
改良された性質、特に線熱膨張率(CLTE)の低下、高い
耐落槍衝撃性、及び良好な耐熱作用性を有するポリマー
ブレンドに関する。上記組成物は耐衝撃性の切欠き脆性
が低下し、完性寸法と平滑仕上げが予想可能である。射
出成形法によって製造される成形体、特に大きい表面を
有する部品の製造に有用である。このような性質は車体
外部パネルに特に望ましい。DETAILED DESCRIPTION OF THE INVENTION The present invention is a novel polymeric mold composition comprising an amorphous polymer matrix and an inorganic filler.
g composition). More particularly, the present invention relates to polymer blends with improved properties, especially reduced coefficient of linear thermal expansion (CLTE), high dart impact resistance, and good thermal activity. The above composition has reduced impact notch brittleness and predictable finish size and smooth finish. It is useful for the production of moldings produced by the injection molding method, in particular parts having a large surface. Such properties are particularly desirable for body exterior panels.
米国特許第4,098,374号はマトリックスインターポリマ
ー、グラフトゴムコポリマー、上記2種類のポリマー以
外の8.5〜13の範囲内の溶解パラメーターを有するポリ
マー及び無機充てん剤から成るブレンドを開示してい
る。ABS樹脂、約14%の粘土及びポリメチルメタクリレ
ートまたはセルロースブチレートから成るこのようなブ
レンドの例が開示されている。この参考文献はブレンド
にポリカーボネートも用いられることをさらに教えてい
る。U.S. Pat. No. 4,098,374 discloses a blend of a matrix interpolymer, a graft rubber copolymer, a polymer other than the above two polymers having a solubility parameter in the range of 8.5 to 13, and an inorganic filler. An example of such a blend consisting of ABS resin, about 14% clay and polymethylmethacrylate or cellulose butyrate is disclosed. This reference further teaches that polycarbonate may also be used in the blend.
日本特許第52/63954号では、ABS樹脂20〜45重量%、ポ
リカーボネート樹脂4.5〜20重量%、及びタルク5〜30
重量%から成るブレンドが開示されている。このような
組成物は適当な熱変形性を有さず、例えば耐落槍衝撃性
または切欠きアイゾット衝撃値によって測定した靴性が
充分でないことが判明している。In Japanese Patent No. 52/63954, ABS resin 20-45 wt%, polycarbonate resin 4.5-20 wt%, and talc 5-30.
Blends consisting of weight percent are disclosed. It has been found that such compositions do not have suitable thermal deformability and, for example, have poor shoe properties as measured by dart impact resistance or notched Izod impact values.
例えば自動車外部射出成形部品のようなある用途では、
1種類のポリマー樹脂に耐低温衝撃性ならびに低い線熱
膨張率及び耐高温たわみ性の全てを与えることが望まし
い。線熱膨張率(ASTM D696によって測定)が21〜49℃
(70〜120゜F)の温度範囲にわたって7.0×10-5/℃(3.
9×10-5/゜F)未満でないかぎり、極端な温度条件が完
成アセンブリの種々な要素の不適合を生じうる。過剰に
膨張するドアまたはフェンダー要素は極端な熱条件にお
いて組立てた完成製品のバックリングまたは不適合を生
ずる。特に低温において熱可塑性樹脂が特に衝撃下のク
ラッキングを受ける場合の耐落槍衝撃性によって測定さ
れる耐衝撃性が同様に重要である。一般に線熱膨張率の
改良は充てん剤量を増加させることによって得られる
が、耐衝撃性、特に耐低温衝撃性はしばしば許容し難い
レベルにまで低下する。例えばガラス繊維のような繊維
強化添加剤はCLTEの低下に非常に効果的であるが、この
ような繊維は生成する物体の表面に目立ち、それによっ
て許容し難い表面特性を生ずる。In some applications, such as automotive exterior injection molded parts,
It is desirable to provide one polymer resin with low temperature impact resistance as well as low coefficient of linear thermal expansion and high temperature flex resistance. Linear thermal expansion coefficient (measured by ASTM D696) 21-49 ℃
7.0 × 10 -5 / ° C (3.
Unless it is less than 9 × 10 -5 / ° F), extreme temperature conditions can result in incompatibility of various elements of the finished assembly. Over-expanding doors or fender elements cause buckling or incompatibility of the assembled finished product in extreme thermal conditions. Impact resistance, as measured by dart impact resistance, especially when the thermoplastic resin undergoes cracking under impact, especially at low temperatures, is also important. Improvements in the coefficient of linear thermal expansion are generally obtained by increasing the amount of filler, but impact resistance, especially low temperature impact resistance, is often reduced to unacceptable levels. Although fiber-reinforced additives such as glass fibers are very effective in lowering the CLTE, such fibers stand out on the surface of the resulting object, thereby producing unacceptable surface properties.
従って、許容できる高い耐落槍衝撃性、特に耐低温落槍
衝撃性と低い切欠き脆性を保持しながら、低い線熱膨張
率を有する改良されたポリマーブレンドが提供されるこ
とが望ましい。Therefore, it is desirable to provide an improved polymer blend having a low coefficient of linear thermal expansion while retaining an acceptable high dart impact resistance, especially low temperature dart impact resistance, and low notch brittleness.
さらに、それから製造した部品が変形なく高温にさらさ
れるように、高い荷重下加熱たわみ温度を保有するよう
な改良されたポリマーブレンドを提供することが望まし
い。Further, it is desirable to provide an improved polymer blend that retains the high heat deflection temperature under load so that the parts made therefrom will be exposed to high temperatures without deformation.
本発明によると、次の成分: (A) 芳香族ポリカーボネート、50〜80重量%、特に
50〜80重量%; (B) ビニル芳香族モノマーのゴム改質ホモポリマー
またはコポリマー、5〜46重量%、好ましくは5〜46重
量%; (C)(i) 最終ブレンド中のタルク又は粘土充てん
剤粒子の少なくとも98重量%が44μm未満の粒径(大き
いサイズ)を有し、(ii) 平均充てん剤粒径対厚さ
(大きいサイズ対小さいサイズ)比4〜24であるように
選択した無機充てん剤、4〜18重量%を含む充てん剤入
りポリマーブレンドを提供する。According to the invention, the following components: (A) aromatic polycarbonate, 50-80% by weight, in particular
50-80 wt%; (B) Rubber-modified homopolymer or copolymer of vinyl aromatic monomer, 5-46 wt%, preferably 5-46 wt%; (C) (i) Talc or clay charge in final blend Inorganic selected such that at least 98% by weight of the agent particles have a particle size (large size) of less than 44 μm and (ii) an average filler particle size to thickness (large size to small size) ratio of 4-24. Fillers Provided are filled polymer blends containing from 4 to 18% by weight.
前記ブレンドは線熱膨張率(CLTE)7.0×10-5/℃(3.9
×10-5/゜F)以下、耐落槍衝撃性〔−29℃(−20゜
F)〕少なくとも11.3ジュール(100インチポンド)及び
455kPa(66psi)におけるASTMD−648−82による荷重下
加熱たわみ温度少なくとも110℃(230゜F)を有する。The blend has a coefficient of linear thermal expansion (CLTE) of 7.0 × 10 -5 / ℃ (3.9
× 10 -5 / ° F) or less, dart impact resistance [−29 ° C (−20 °
F)] at least 11.3 Joules (100 inch pounds) and
It has a heat deflection temperature under load according to ASTM D-648-82 at 455 kPa (66 psi) of at least 110 ° C (230 ° F).
CLTEの測定に用いた方法はASTM D696の方法である。落
槍衝撃強さは速度2.2m/秒(5mile/時)槍直径1.3cm(0.
5インチ)による、ASTM D3763−86に従って測定した機
器による落槍衝撃強さである。The method used for measuring CLTE is the method of ASTM D696. Drop dart impact strength is 2.2m / sec (5mile / hr) Spear diameter 1.3cm (0.
5 inch) dart impact strength by the instrument measured according to ASTM D3763-86.
本発明によって有効に用いられる芳香族ポリカボネート
樹脂は今までに公知であり、先行技術に述べられてい
る。さらに詳しくは、このような樹脂には塩化メチレン
と例えばアルカリ金属水酸化物またはピリジンのような
酸結合剤の存在下でジヒドロキシアリール化合物、特に
ビスジヒドロキシアリールアルカンをホスゲンまたはビ
スクロロホルメートと共に界面重合または溶液重合する
ことによって得られるポリカーボネート樹脂がある。特
に良好に敵する芳香族ポリカーボネートには、ビスフェ
ノールAポリカーボネート、テトラブロモビスフェノー
ルAポリカーボネート、テトラメチルビスフェノールA
ポリカーボネート、1,1−ビス(4−ヒドロキシフェニ
ル)−1−フェニルエタンポリカーボネート及びこれら
の混合物がある。Aromatic polycarbonate resins usefully employed in accordance with the present invention are known to date and described in the prior art. More specifically, such resins include interfacial polymerization of dihydroxyaryl compounds, especially bisdihydroxyarylalkanes, with phosgene or bischloroformate in the presence of methylene chloride and an acid binder such as an alkali metal hydroxide or pyridine. Alternatively, there is a polycarbonate resin obtained by solution polymerization. Particularly suitable aromatic polycarbonates include bisphenol A polycarbonate, tetrabromobisphenol A polycarbonate, and tetramethylbisphenol A.
There are polycarbonates, 1,1-bis (4-hydroxyphenyl) -1-phenylethane polycarbonate and mixtures thereof.
ビニル芳香族モノマーのゴム改質ホモポリマーとコポリ
マーには、スチレンもしくはα−メチルスチレンのゴム
改質ホモポリマーまたはスチレンもしくはα−メチルス
チレンと共重合可能なコモノマーとのゴム改質コポリマ
ーがある。好ましいコモノマーには単独でまたは特にメ
チルメタクリレート、メタクリロニトリル、フマロニト
リル及び/または例えばN−フェニルマレイミドのよう
なN−アリールマレイミドのような他のコモノマーと組
合せて用いられるアクリロニトリルがある。好ましいコ
ポリマーには、スチレン70〜90%、好ましくは70〜80%
とアクリロニトリル30〜10%、好ましくは30〜20%を含
む。Rubber-modified homopolymers and copolymers of vinyl aromatic monomers include rubber-modified homopolymers of styrene or α-methylstyrene or rubber-modified copolymers of comonomers copolymerizable with styrene or α-methylstyrene. Preferred comonomers are acrylonitrile used alone or in particular in combination with methylmethacrylate, methacrylonitrile, fumaronitrile and / or other comonomers such as N-arylmaleimides such as N-phenylmaleimide. Preferred copolymers include 70-90% styrene, preferably 70-80%
And acrylonitrile 30 to 10%, preferably 30 to 20%.
適当なゴムには、共役ジェン特にブタジェンの周知のホ
モポリマートコポリマー;ならびに例えばオレフィンポ
リマー、特にエチレン、プロピレンのコポリマー;及び
任意に非共役ビェンまたはアクリレートラバー、特に炭
素数4〜6のアルキル基を有するアルキルアクリレート
のホモポリマーまたはコポリマーがある。さらに、上記
ラバーポリマーの混合物も任意に用いることができる。
好ましいゴムはブタジェンホモポリマー及びブタジェン
と約30重量%までのスチレンとのコポリマーである。こ
のようなコポリマーはランダムコポリマーまたはブロッ
クコポリマーであり、さらに残留不飽和を除くために水
素化することができる。Suitable rubbers include the well-known homopolymeric copolymers of conjugated gens, especially butadiene, as well as, for example, olefin polymers, especially copolymers of ethylene, propylene; There are homopolymers or copolymers of alkyl acrylates having. Further, a mixture of the above rubber polymers can be optionally used.
The preferred gums are butadiene homopolymers and copolymers of butadiene and styrene up to about 30% by weight. Such copolymers are random or block copolymers and can be further hydrogenated to remove residual unsaturation.
ゴム改質コポリマーは、ゴムポリマーの存在下でのコポ
リマーの塊状重合、溶液重合または乳化重合のようなグ
ラフト発生方法によって製造することが好ましい。The rubber modified copolymer is preferably produced by a graft generation method such as bulk polymerization, solution polymerization or emulsion polymerization of the copolymer in the presence of the rubber polymer.
ゴム基幹のグラフトコポリマーを形成するための乳化重
合では、グラフト化したコポリマーを含む大小のゴム粒
子を製造するために凝集テクノロジーあ用いることが技
術上周知である。このプロセス中ではコポリマーの非グ
ラフト化、マトリックスの種々な量も形成される。ビニ
ル芳香族モノマーのゴム改質コポリマーの溶液重合また
は塊状重合では、マトリックスコポリマーが形成され
る。このマトリックスはさらに、それにグラフト化した
またはその中に閉塞されたコポリマーを有するゴム粒子
を含む。In emulsion polymerization to form rubber-based graft copolymers, it is well known in the art to use aggregation techniques to produce large and small rubber particles containing the grafted copolymer. During this process, non-grafted copolymer, various amounts of matrix are also formed. In solution or bulk polymerization of rubber modified copolymers of vinyl aromatic monomers, matrix copolymers are formed. The matrix further comprises rubber particles having the copolymer grafted thereto or occluded therein.
特に好ましい製品には、塊状重合したもしくは溶液重合
したゴム改質コポリマーと付加的な量の乳化重合した、
好ましくは凝集したゴム改質コポリマーの両方から成
り、2型式の粘度分布を含むゴム改質コポリマーブレン
ドがある。最も好ましいゴム改質コポリマーはブタジエ
ンラバー改質コポリマーである。スチレンとアクリロニ
トリルのブタジエンゴム改質コポリマーは、技術上ABS
樹脂と呼ばれる。Particularly preferred products include bulk polymerized or solution polymerized rubber-modified copolymers and an additional amount of emulsion polymerized,
There are rubber modified copolymer blends that preferably consist of both agglomerated rubber modified copolymers and that include a type 2 viscosity distribution. The most preferred rubber modified copolymer is a butadiene rubber modified copolymer. The butadiene rubber modified copolymer of styrene and acrylonitrile is technically ABS
Called resin.
本発明の必要条件を満たす生成ポリマーブレンドを得る
には、細長い構造を有する適当なタルク又は粘土充てん
剤の特定の濃度を用いることが望ましい。球状充てん剤
は細長い充てん剤に比べて、生成ポリマーブレンドのCL
TEを低下させる能力を有さないことが今回発見された。
充てん剤の大きいサイズ/小さいサイズ(直径/厚さ)
比の測定は、凍結ミクローミングによって薄い切片を最
初に作成し、3000〜15000倍率の電子顕微鏡写真を撮る
ことによって最も良く実施される。To obtain a resulting polymer blend that meets the requirements of the present invention, it is desirable to use a particular concentration of a suitable talc or clay filler having an elongated structure. Spherical fillers are better than elongated fillers in CL of polymer blends produced.
It has now been discovered that it does not have the ability to reduce TE.
Large / small size of packing (diameter / thickness)
Ratio determinations are best performed by first making thin sections by freeze micromming and taking electron micrographs at 3000-15000 magnification.
少なくとも25個、好ましくは50個の充てん剤粒子の典型
的なサンプルの直径/厚さを測定することによって、直
径/厚さ比の比較的正確な値を得ることができる。40μ
m未満の直径のタルク又は粘土充てん剤の割合は325メ
ッシュスクリーンを用いるスクリーン分析によって測定
することができる。この代りに、充てん剤の平均粒度と
40μm未満及び20μm未満の充てん剤の割合は沈降分析
法の使用によって測定することができる。ASAE会報(Tr
ansaction of ASAE)491頁(1983)参照。By measuring the diameter / thickness of a typical sample of at least 25, preferably 50, filler particles, a relatively accurate value of the diameter / thickness ratio can be obtained. 40μ
The percentage of talc or clay filler with a diameter less than m can be measured by screen analysis using a 325 mesh screen. Instead of the average particle size of the filler
The proportion of fillers below 40 μm and below 20 μm can be measured by the use of sedimentation analysis. ASAE Bulletin (Tr
ansaction of ASAE) 491 (1983).
本発明による好ましい組成物は、1種類以上のタルク又
は粘土充てん剤5〜15%、好ましくは6〜12%を含む組
成物である。特に好ましい充てん剤では、充てん剤の少
なくとも99重量%が20μm未満の平均粒径を有する。A preferred composition according to the invention is a composition comprising 5 to 15%, preferably 6 to 12% of one or more talc or clay fillers. In a particularly preferred filler, at least 99% by weight of the filler has an average particle size of less than 20 μm.
上記方法によって測定して6〜18の平均直径/厚さの比
を有する充てん剤を含む組成物が非常に好ましい。充て
ん剤は遊離金属酸化物の含量が非常に低い非焼成タルク
及び粘土である。Highly preferred are compositions containing fillers having an average diameter / thickness ratio of 6 to 18 as measured by the above method. Fillers are uncalcined talc and clay with a very low content of free metal oxides.
本発明による好ましい組成物は芳香族ポリマーカーボネ
ート55〜75重量%と、ゴム改質ホモポリマーまたはコポ
リマー10〜40重量%とを有し、少なくとも22.6ジュール
(200インチポンド)の−29℃(−20゜F)における落槍
衝撃値、6.7×10-5/℃(3.7+10-5/゜F)未満のCLTE、
及び少なくとも121℃(250゜F)のDTULを有する。Preferred compositions according to the present invention have 55 to 75 wt% aromatic polymer carbonate and 10 to 40 wt% rubber modified homopolymer or copolymer, and have at least 22.6 joules (200 inch pounds) of -29 ° C (-20%). dart impact value in ° F), 6.7 × 10 -5 /℃(3.7+10 -5 / ° F) of less than CLTE,
And a DTUL of at least 121 ° C (250 ° F).
上記成分A、B、Cをブレンドすることによって、組成
物が製造される。適当な押出機または他の溶融配合装置
において溶融配合する前に、成分を最初に混合または乾
式配合することが望ましい。成分は如何なる順序でも結
合し、配合することができる。上記成分の他に、米国特
許第4,528,303号に開示されている多官能性有機ケイ素
化合物のようなカップリング剤等の付加的な添加剤をブ
レンドに含めることができる。顔料、酸化防止剤、加工
助剤、難燃剤、滑剤、離型剤、及び他の添加剤をも組成
物に含めることができる。The composition is produced by blending the above components A, B, C. It may be desirable to first mix or dry compound the components prior to melt compounding in a suitable extruder or other melt compounding equipment. The components can be combined and combined in any order. In addition to the above components, the blend can include additional additives such as coupling agents such as the polyfunctional organosilicon compounds disclosed in US Pat. No. 4,528,303. Pigments, antioxidants, processing aids, flame retardants, lubricants, mold release agents, and other additives can also be included in the composition.
一般に多量のポリカーボネートの添加は改良されたDTUL
を有する最終組成物を生ずる。しかし、過剰量のポリカ
ーボネートの使用は落槍衝撃強さの低下を生ずる。本発
明の樹脂ブレンドから製造される射出成形成分は一般に
予想外に平滑で、欠陥のない表面仕上げを有し、耐衝撃
性試験において低い切欠き脆性であることが判明してい
る。さらに組成物はポリカーボネート樹脂に比べて、例
えばガソリンのような炭化水素溶剤に対する改良された
耐性を示す。Generally, the addition of large amounts of polycarbonate is improved DTUL
Resulting in a final composition having However, the use of excessive amounts of polycarbonate results in reduced dart impact strength. Injection-molded components made from the resin blends of the present invention are generally found to be unexpectedly smooth, have a defect-free surface finish, and have low notch brittleness in impact testing. Further, the composition exhibits improved resistance to hydrocarbon solvents such as gasoline, as compared to polycarbonate resins.
上記成分の他に、ポリマーブレンドに付加的な非晶質ポ
リマーをさらに配合することができる。本発明の組成物
にさらに配合することのできる付加的なポリマー成分の
例は熱可塑性ポリウレタン、非晶質ポリエステル及びポ
リアリーレート樹脂を含む。In addition to the above components, additional amorphous polymers can be further incorporated into the polymer blend. Examples of additional polymer components that can be further incorporated into the compositions of the present invention include thermoplastic polyurethanes, amorphous polyesters and polyarylate resins.
本発明を説明したが、次の実験は本発明をさらに説明す
るものであり、本発明を限定するものとは解釈すべきで
はない。部と%は重量に基づくものである。Having described the invention, the following experiments further illustrate the invention and should not be construed as limiting the invention. Parts and percentages are by weight.
実験 1.ラン1〜4、比較例a ビスフェノールAポリカーボネート64重量%、塊状重合
ポリブタジエン改質ABS樹脂(ゴム20%、アクリロニト
リル23%、スチレン57%を含む)36重量%を含むポリカ
ーボネート/ABSブレンドを循環空気乾燥装置において99
℃で4時間乾燥させてから、ポリエチレンバッグ内でエ
ポキシ化大豆油0.1%、トリスノニルフェニルホスフィ
ット(TNPP)0.1%及び種々な量の非焼成粘土〔アング
ローアメリカン クレイ カンパニー(Anglo−Amerian
Clay Company)から入手可能あテックス(Tex)10R〕
と混合した。混合物をワーナー フライダーラー(Warn
er Pfleiderer)ZSK−30二軸スクリュー押出機を通して
押出成形した。加熱装置を270℃(518゜F)に維持し、
スクリューは400rpmでランさせ、スループット速度は約
13.6kg/時(30lb/時)であった。ストランドを水浴中で
冷却し、チョップした。次に課粒を循環空気炉中で99℃
(210゜F)において4時間乾燥させ、アルブルグ(Arbu
rg)28トン射出成形機内で溶融物温度288℃(550゜F)
及び型温度82℃(180゜F)において試験片に成形した。
得られた射出成形サンプルの物理的性質を次に測定し
た。得られたブレンド中で粒子の99.99%より多くが44
μm未満の直径を有した。平均粒径/厚さは14.3であっ
た。試験結果は第1表に示す。Experiment 1. Runs 1-4, Comparative Example a A polycarbonate / ABS blend containing 64% by weight of bisphenol A polycarbonate, 36% by weight of bulk polymerized polybutadiene modified ABS resin (including 20% rubber, 23% acrylonitrile and 57% styrene). 99 in circulating air dryers
After drying at ℃ for 4 hours, in a polyethylene bag 0.1% epoxidized soybean oil, 0.1% trisnonylphenylphosphite (TNPP) and various amounts of uncalcined clay [Anglo-Amerian
Available from Clay Company) Tex 10R]
Mixed with. Mix the mixture with Warner
er Pfleiderer) ZSK-30 twin screw extruder. Keep the heating device at 270 ° C (518 ° F),
The screw runs at 400 rpm and the throughput speed is about
It was 13.6 kg / hour (30 lb / hour). The strand was cooled in a water bath and chopped. Next, the grain is placed in a circulating air oven at 99 ° C.
Dry for 4 hours at (210 ° F) and
rg) Melt temperature 288 ° C (550 ° F) in a 28 ton injection molding machine
The test pieces were molded at a mold temperature of 82 ° C (180 ° F).
The physical properties of the resulting injection molded sample were then measured. More than 99.99% of the particles in the resulting blend are 44
It had a diameter of less than μm. The average particle size / thickness was 14.3. The test results are shown in Table 1.
実験 2.ラン5、比較例b 実験1に用いたポリカーボネート/ABSブレンドに第2表
に示した直径/厚さ比を有する2種類の粘土サンプル各
6%を配合した。これらの組成物も実験1の方法に実質
的に従って成形した。試験結果は第2表に示す。平均粒
径/厚さ比16.3を有する粘土を含む組成物は、平均粒径
/厚さ比2.8を有する粘土を含む組成物のCLTE7.8×10-5
/℃(4.28×10-5/゜F)に比べて、CLTE6.6×10-5/℃
(3.65×10-5/゜F)を有した。全てのサンプルが好まし
いDTULと−29℃(−20゜F)での落槍衝撃強さを有す
る。 Run 2. Run 5, Comparative Example b The polycarbonate / ABS blend used in Run 1 was compounded with 6% each of two clay samples having the diameter / thickness ratios shown in Table 2. These compositions were also molded substantially according to the method of Experiment 1. The test results are shown in Table 2. A composition comprising clay having an average particle size / thickness ratio of 16.3 is a CLTE 7.8 × 10 −5 of a composition comprising clay having an average particle size / thickness ratio of 2.8.
CLTE 6.6 × 10 -5 / ° C compared to / ° C (4.28 × 10 -5 / ° F)
(3.65 × 10 -5 / ° F). All samples have preferred DTUL and dart impact strength at -29 ° C (-20 ° F).
充てん剤の直径(測定可能な2サイズの中の最大サイ
ズ)と充てん剤の厚さ(最小サイズ)を、充てん剤相を
強調するように暴露させた射出成形サンプルのミクロト
ームスライスの透過電子顕微鏡写真(7500X)から測定
した。充てん剤の直径と厚さは20〜50粒子のサンプルサ
イズに対して手動で測定した。Transmission electron micrograph of a microtome slice of an injection-molded sample in which the packing diameter (maximum size out of two measurable sizes) and packing thickness (minimum size) were exposed to emphasize the packing phase. (7500X). Filler diameter and thickness were measured manually for sample sizes of 20-50 particles.
実験 3.ラン5−13 実験1と同じやり方で、ポリカーボネート/ABSブレンド
に全ての粒子の>99.99%が44μm未満を有する多くの
種類のタルクを配合した。これらのサンプルの試験結果
を第3表に示す。タルク6〜10%を含む全てのサンプル
は好ましい値のCLTEと−29℃(−20゜F)の落槍衝撃強
さを有する。 Run 3. Run 5-13 In the same manner as Run 1, a polycarbonate / ABS blend was compounded with many types of talc with> 99.99% of all particles less than 44 μm. The test results of these samples are shown in Table 3. All samples containing 6-10% talc have favorable values for CLTE and dart impact strength of -29 ° C (-20 ° F).
実験 4.ラン14,15,比較例c,d 実験1からのポリカーボネートとABS樹脂とのブレンド
に6〜10%の量で4種類のタルクを配合した。落槍衝撃
試験とCLTEは生成ブレンドと非改質ポリカーボネート/A
BSブレンドの12.5×12.5cm(5×5インチ)プラック上
で実験した。4種類の充てん剤はMP−50−26(D/T=6.
2,<44μm粒子98%;<20μm粒子83%、l1)ラン14;M
P25−38(D/T=9.5,<44μm粒子99.99%;<20μm粒
子99.5%,l2)ラン15;MP99−10(D/T=5.7,<44μm粒
子、77%;<20μm粒子58%l3)比較例C:及びMP99−54
(D/T=1.8,<44μm粒子98.0%;<20μm粒子67%,
l4)比較例dであった。全てのタルクはファイザーから
得た。全てのサンプルのDTUL値は124℃(255゜F)であ
った。CLTEと−29℃(−20゜F)における耐落槍衝撃性
はそれぞれ第1図と第2図に示す。 Experiment 4. Runs 14, 15, Comparative Examples c, d Four blends of talc were blended into the blend of polycarbonate from Experiment 1 and ABS resin in an amount of 6-10%. Drop dart impact test and CLTE produced blends and unmodified polycarbonate / A
Experiments were performed on BS blended 12.5 x 12.5 cm (5 x 5 inch) plaques. The four types of packing are MP-50-26 (D / T = 6.
2, <44 μm particles 98%; <20 μm particles 83%, l 1 ) Run 14; M
P25-38 (D / T = 9.5, <44 μm particles 99.99%; <20 μm particles 99.5%, l 2 ) Run 15; MP99-10 (D / T = 5.7, <44 μm particles, 77%; <20 μm particles 58% l 3 ) Comparative Example C: and MP99-54
(D / T = 1.8, <44μm particles 98.0%; <20μm particles 67%,
l 4 ) Comparative example d. All talc was obtained from Pfizer. The DTUL value for all samples was 124 ° C (255 ° F). CLTE and dart impact resistance at -29 ° C (-20 ° F) are shown in Figures 1 and 2, respectively.
第1図と第2図への参照からわかるように、充てん剤の
割合を高めるとCLTEが低下した生成物が得られるが、落
槍衝撃強さも低下する。ある種の充てん剤はCLTE3.9未
満と落槍衝撃値−29℃(−20゜F)少なくとも11.3ジュ
ール(100lb)の同時必要条件を満たすことができな
い。As can be seen from the reference to FIGS. 1 and 2, increasing the proportion of filler results in a product with reduced CLTE, but also with dart impact strength. Certain packings cannot meet the simultaneous requirements of CLTE 3.9 and dart impact value of -29 ° C (-20 ° F) of at least 11.3 Joules (100lb).
実験 5,ラン16〜22,比較例e N−フェニルマレイミド改質ABS樹脂とエマルジョョンA
BS樹脂にポリカーボネートを配合した。N−フェニルマ
レイミド改質ABS樹脂はAN 19%,ブタジエン6.5%,ス
チレン1.3%及びN−フェニルマレイミド11.5%を含
み、溶解したポリブタジエンゴムの存在下でのモノマー
の溶液重合によって製造した。次に、このABSにスチレ
ン/アクリロニトリル(50/50)コポリマーをグラフト
化したポリブタジエンゴム50%を含むエマルジョンABS
20%を配合した。ポリカーボネートは溶融流量(melt f
low rate)を有するビスフェノールAポリカーボネート
〔ダウ ケミカルカンパニー(Dow Chemical Company)
から入手可能なキャリバー(CALIBRETM)300−10〕であ
った。Experiment 5, Runs 16 to 22, Comparative Example e N-Phenylmaleimide Modified ABS Resin and Emulsion A
Polycarbonate was blended with BS resin. The N-phenylmaleimide modified ABS resin contained 19% AN, 6.5% butadiene, 1.3% styrene and 11.5% N-phenylmaleimide and was prepared by solution polymerization of monomers in the presence of dissolved polybutadiene rubber. Next, emulsion ABS containing 50% of polybutadiene rubber obtained by grafting styrene / acrylonitrile (50/50) copolymer on this ABS.
20% was compounded. Polycarbonate has a melt flow rate (melt f
bisphenol A polycarbonate with low rate [Dow Chemical Company
Caliber (CALIBRE ™ 300-10) available from
種々な粘土とタルク充てん剤は4〜10重量%の量でポリ
マーに混入する。結果は第4表に示す。Various clay and talc fillers are incorporated into the polymer in amounts of 4-10% by weight. The results are shown in Table 4.
第1図はCLTEと、実験4で定義した4種類の充てん剤に
関する充てん剤添加量との関係を示す; 第2図は落槍衝撃強さと、実験4で定義した4種類の充
てん剤に関する充てん剤添加量との関係を示す。Fig. 1 shows the relationship between CLTE and the amount of filler added for the four fillers defined in Experiment 4; Fig. 2 shows the dart impact strength and the fillers for the four fillers defined in Experiment 4. The relationship with the amount of agent added is shown.
Claims (8)
またはコポリマー、5〜46重量%;及び (C)(i)最終ブレンド中の充てん剤粒子の少なくと
も98重量%が44μm未満の粒径を有し; (ii)平均の充てん剤粒径/厚さ比が4〜24であるよう
に選択したタルク又は粘土充てん剤、4〜18重量%; を含む、線熱膨張率(CLTE)、7.0×10-5/℃(3.9×10
-5/゜F)以下、−29℃(−20゜F)における落槍衝撃強
さ少なくとも11.3ジュール(100インチポンド)及び66p
si(455KPa)での荷重下加熱たわみ温度(DTUL)少なく
とも110℃(230゜F)を有する充てん剤入りポリマーブ
レンド。1. The following components: (A) aromatic polycarbonate, 50-80% by weight; (B) rubber-modified homopolymer or copolymer of vinyl aromatic monomer, 5-46% by weight; and (C) (i. ) At least 98% by weight of the filler particles in the final blend have a particle size of less than 44 μm; (ii) a talc or clay filler selected such that the average filler particle size / thickness ratio is 4-24. Thermal expansion coefficient (CLTE), 7.0 × 10 −5 / ° C. (3.9 × 10
-5 / ° F) or less, -29 ° C (-20 ° F) dart impact strength of at least 11.3 Joules (100 in-lbs) and 66p
A filled polymer blend having a heat deflection temperature (DTUL) of at least 110 ° C (230 ° F) under load at si (455 KPa).
下を有する請求項1記載のポリマーブレンド。Wherein CLTE 6.7 × 10 -5 /℃(3.7×10 -5 / ° F) the polymer blend of claim 1 having the following.
くとも22.6ジュール(200インチポンド)を有する請求
項1記載のポリマーブレンド。3. The polymer blend of claim 1 having a dart impact strength at −29 ° C. (−20 ° F.) of at least 22.6 joules (200 inch pounds).
満の粒径を有する請求項1記載のポリマーブレンド。4. The polymer blend of claim 1 wherein at least 99% of the filler particles have a particle size less than 20 μm.
る請求項1記載のポリマーブレンド。5. The polymer blend of claim 1 in which the filler has an average diameter / thickness ratio of 6-18.
から選択する請求項1記載のポリマーブレンド。6. The polymer blend of claim 1 wherein the filler is selected from the group consisting of talc and green clay.
ニトリルのコポリマー及び任意にN−フェニルマレイミ
ドを含み、そのゴムがブタジェンのホモポリマーもしく
はコポリマー、またはエチレン、ブロピレン及び非共役
ジェンのインターポリマーである請求項1記載のポリマ
ーブレンド。7. A rubber-modified copolymer comprising a copolymer of styrene and acrylonitrile and optionally N-phenylmaleimide, the rubber being a homopolymer or copolymer of butadiene, or an interpolymer of ethylene, bropyrene and a non-conjugated gen. 1. The polymer blend according to 1.
工品。8. A processed article comprising the polymer blend of claim 1.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US334411 | 1989-04-07 | ||
US07/334,411 US5091461A (en) | 1989-04-07 | 1989-04-07 | Filled polymeric blend |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02294358A JPH02294358A (en) | 1990-12-05 |
JPH0733473B2 true JPH0733473B2 (en) | 1995-04-12 |
Family
ID=23307082
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2091943A Expired - Lifetime JPH0733473B2 (en) | 1989-04-07 | 1990-04-06 | Filled polymer blend |
Country Status (7)
Country | Link |
---|---|
US (1) | US5091461A (en) |
EP (1) | EP0391413B1 (en) |
JP (1) | JPH0733473B2 (en) |
KR (1) | KR0145067B1 (en) |
CA (1) | CA2014012C (en) |
DE (1) | DE69029338T2 (en) |
MX (1) | MX165089B (en) |
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-
1989
- 1989-04-07 US US07/334,411 patent/US5091461A/en not_active Expired - Lifetime
-
1990
- 1990-04-05 EP EP90106536A patent/EP0391413B1/en not_active Expired - Lifetime
- 1990-04-05 DE DE69029338T patent/DE69029338T2/en not_active Expired - Fee Related
- 1990-04-06 JP JP2091943A patent/JPH0733473B2/en not_active Expired - Lifetime
- 1990-04-06 MX MX20238A patent/MX165089B/en unknown
- 1990-04-06 KR KR1019900004722A patent/KR0145067B1/en not_active IP Right Cessation
- 1990-04-06 CA CA002014012A patent/CA2014012C/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
KR900016370A (en) | 1990-11-13 |
EP0391413A3 (en) | 1992-02-26 |
EP0391413A2 (en) | 1990-10-10 |
EP0391413B1 (en) | 1996-12-11 |
CA2014012C (en) | 2001-08-21 |
DE69029338D1 (en) | 1997-01-23 |
AU630180B2 (en) | 1992-10-22 |
AU5298690A (en) | 1990-10-11 |
KR0145067B1 (en) | 1998-07-15 |
US5091461A (en) | 1992-02-25 |
CA2014012A1 (en) | 1990-10-07 |
JPH02294358A (en) | 1990-12-05 |
MX165089B (en) | 1992-10-21 |
DE69029338T2 (en) | 1997-06-05 |
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